EP0088964A2 - Process for preparing insoluble, only slightly expandable polymers of basic vinyl-heterocyclic compounds, and their use - Google Patents

Process for preparing insoluble, only slightly expandable polymers of basic vinyl-heterocyclic compounds, and their use Download PDF

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EP0088964A2
EP0088964A2 EP83102132A EP83102132A EP0088964A2 EP 0088964 A2 EP0088964 A2 EP 0088964A2 EP 83102132 A EP83102132 A EP 83102132A EP 83102132 A EP83102132 A EP 83102132A EP 0088964 A2 EP0088964 A2 EP 0088964A2
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polymers
parts
polymerization
vinyl
water
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EP0088964A3 (en
EP0088964B1 (en
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Walter Denzinger
Hans-Helmut Dr. Goertz
Axel Dr. Sanner
Heinrich Dr. Hartmann
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BASF SE
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    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
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    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
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    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
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    • B01J31/06—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing polymers
    • B01J31/08—Ion-exchange resins
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    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/165—Polymer immobilised coordination complexes, e.g. organometallic complexes
    • B01J31/1658—Polymer immobilised coordination complexes, e.g. organometallic complexes immobilised by covalent linkages, i.e. pendant complexes with optional linking groups, e.g. on Wang or Merrifield resins
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J39/00—Cation exchange; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
    • B01J39/08—Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
    • B01J39/16—Organic material
    • B01J39/18—Macromolecular compounds
    • B01J39/20—Macromolecular compounds obtained by reactions only involving unsaturated carbon-to-carbon bonds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F26/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen
    • C08F26/06—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen by a heterocyclic ring containing nitrogen
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    • C12N11/00—Carrier-bound or immobilised enzymes; Carrier-bound or immobilised microbial cells; Preparation thereof
    • C12N11/02—Enzymes or microbial cells immobilised on or in an organic carrier
    • C12N11/08—Enzymes or microbial cells immobilised on or in an organic carrier the carrier being a synthetic polymer
    • C12N11/082—Enzymes or microbial cells immobilised on or in an organic carrier the carrier being a synthetic polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds
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    • C12N11/00—Carrier-bound or immobilised enzymes; Carrier-bound or immobilised microbial cells; Preparation thereof
    • C12N11/02—Enzymes or microbial cells immobilised on or in an organic carrier
    • C12N11/08—Enzymes or microbial cells immobilised on or in an organic carrier the carrier being a synthetic polymer
    • C12N11/082—Enzymes or microbial cells immobilised on or in an organic carrier the carrier being a synthetic polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C12N11/087—Acrylic polymers
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    • B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
    • B01J2231/30—Addition reactions at carbon centres, i.e. to either C-C or C-X multiple bonds
    • B01J2231/32—Addition reactions to C=C or C-C triple bonds
    • B01J2231/321—Hydroformylation, metalformylation, carbonylation or hydroaminomethylation
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    • B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/10—Complexes comprising metals of Group I (IA or IB) as the central metal
    • B01J2531/16—Copper
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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    • B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/80—Complexes comprising metals of Group VIII as the central metal
    • B01J2531/82—Metals of the platinum group
    • B01J2531/824—Palladium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/18—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
    • B01J31/1805—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing nitrogen
    • B01J31/181—Cyclic ligands, including e.g. non-condensed polycyclic ligands, comprising at least one complexing nitrogen atom as ring member, e.g. pyridine

Definitions

  • homopolymers of N-vinylimidazoles and vinylpyridines and their copolymers with N-vinyllactams are readily soluble in water and numerous organic solvents. It is also known that insoluble but swellable polymers of vinylimidazoles or vinylpyridines can be prepared by customizing the vinyl heterocycles in the presence of polyfunctional monomers (with two or more copolymerizable double bonds) which have a crosslinking action and, if appropriate, monounsaturated Comonomer polymerized with the addition of radical formers as starters (or initiators).
  • crosslinkers are, for example, divinyl esters of dicarboxylic acids such as succinic acid and adipic acid, diacrylates of polyhydric alcohols such as ethylene glycol and butanediol, allyl ethers of polyhydric alcohols such as pentaerythritol triallyl ether.
  • Crosslinkers of this type are not very easy to prepare and are therefore relatively expensive compared to monounsaturated monomers. Even when larger amounts of the multifunctional monomer are used, the swellability of the polymers in water is relatively high, so that a gel is formed during the polymerization in aqueous solution.
  • US Pat. No. 2,878,183 teaches the production of very strongly crosslinked and therefore insoluble but nevertheless highly swellable polyvinylimidazoles by radical polymerization of N-vinylimidazoles in the presence of large amounts of polyfunctional monomers, the polymerization being carried out in water and the polymers as gels attack.
  • Such highly swellable gels have both in their manufacture 'As with general handling and when used as an ion exchanger or as a carrier for reagents such as enzymes and the like.
  • Serious disadvantages they clog the vessel during manufacture, cannot be stirred or poured out, and large amounts of solvent have to be evaporated during drying. For use, they must be pre-swollen and are not pourable in this state; a column filled with it tends to clog.
  • DE-AS 19 29 501 describes the preparation of copolymers from N-vinyl lactams with small amounts of N-vinylimidazoles by radical polymerization in the presence of crosslinking agents, the polymerization being carried out in 10 to 20% strength aqueous salt solutions.
  • the polymers are then obtained in the form of granules with a diameter of 1 to 7 mm.
  • Disadvantages of this method include in that the isolation of the polymers in pure form from the salt solution is very complex and that the polymer is obtained in coarse, non-porous form and with a relatively small surface area.
  • DE-OS 23 24 204 describes a method for producing poly-N-vinylimidazoles, the polymerization being carried out in an organic solvent and it being very complex to isolate the polymers in solvent-free form.
  • DE-OS 25 06 085 teaches the polymerization of vinylimidazoles without the use of solvents by photoinitiation. Since the polymers are obtained as films, their use is severely restricted. Apart from weaknesses in production, these polymers are only suitable to a limited extent as ion exchangers or carriers for proteins due to their relatively strong swellability.
  • a method for producing relatively weak swellable polymers, even without the addition of greater amounts of crosslinker is, inter alia, in the literature as popcorn polymerization (HF Kauffmann and JW Schunbach, Angew Makromol Ch 45 (1975), 167-175... N-vinylpyrrolidone and Popcorn - polymers; JW Schunbach, HF Kauffmann and G. Zwilling, Makromol. Ch. 177 (1976), 2787 to 2792: acrylic acid popcorn polymers) or in English also as proliferous polymerization (W. Schunbach, Encycl. Of Polymer Sci. And Technol. Vol. 11, 587 to 597).
  • This type of polymerization known in the art as a source of interference, generally leads to technically unusable, irregularly coarse-particle products. It is not yet known for basic vinyl heterocycles.
  • the invention was based on the task of producing porous granular, water-swellable, non-gel-forming basic polymers in the simplest possible manner and using the smallest possible amount of (expensive) crosslinkers with two or more copolymerizable double bonds, which as ion exchangers and as adsorber resins ( Carrier), in particular for proteins (especially enzymes).
  • the polymers obtainable according to the invention differ from the "normal”, that is to say with the aid of customary amounts of free radical formers as starters or polymers obtained by photoinitiation not only in that they swell considerably less in water at the same crosslinker concentration, so that the amount of water taken up by swelling is less than half, usually a third to a seventh or even less, but also in, " overall course of the polymerization and above all in its optical (macro- and microscopic) appearance: a" normal "polymerization without solvent results in a solid block, and in aqueous solution if the monomer and polymer are water-soluble (as in the present case) a gel, while in both cases a porous, granular mass with a grain diameter in the range of about 10 to 500 pm is formed.
  • the grains bake into a porous cake which can be easily crumbled. If the mixture is stirred during the polymerization, whatever it is preferable that the grains agglomerate loosely into irregularly shaped crumbs, the average size of which depends on the intensity of stirring and is usually in the order of 0.1 to 5 mm in diameter.
  • the polymerization of the monomer / crosslinker mixture begins as soon as the atmospheric oxygen has been completely removed, spontaneously even at room temperature and even without the polymerization inhibitors, for example hydroquinone, t-butylpyrocatechol or phenothiazine, which the monomers normally contain to increase their shelf life, would have been removed .
  • the polymerization inhibitors for example hydroquinone, t-butylpyrocatechol or phenothiazine, which the monomers normally contain to increase their shelf life, would have been removed .
  • Molecular oxygen appears to be the only inhibitor that not only inhibits normal radical polymerization but also the polymerization according to the invention.
  • the crosslinking agent is used in amounts of 0.1 to 10, preferably 1 to 4%, based on the total monomer weight.
  • Suitable crosslinkers are those which contain two or more copolymerizable groups in the molecule.
  • Alkylenebisacrylamides such as methylenebisacrylamide and N, N'-bisacryloylethylenediamine, in addition N, N'-divinylethylene urea, N, N'-divinylpropylene urea, ethylidene-bis-3- (N-vinylpyrrolidone) and N, N'-divinyldimididazolyl ( 2,2 ') and 1,1 1- bis (3,3'-vinylbenzimidazolid-2 - one) -1,4-butane.
  • crosslinking agents are, for example, alkylene glycol di (meth) acrylates such as ethylene glycol di (meth) acrylate and tetramethylene glycol di (meth) acrylate, aromatic divinyl compounds such as divinylbenzene and divinyltoluene, and allyl acrylate, divinyldioxane, pentaerythritol triallyl ether and mixtures thereof.
  • alkylene glycol di (meth) acrylates such as ethylene glycol di (meth) acrylate and tetramethylene glycol di (meth) acrylate
  • aromatic divinyl compounds such as divinylbenzene and divinyltoluene
  • allyl acrylate divinyldioxane
  • pentaerythritol triallyl ether pentaerythritol triallyl ether and mixtures thereof.
  • the comonomers which can be polymerized in amounts of up to 30, preferably up to 20,% by weight, based on the total monomer mixture.
  • examples include styrene, acrylic ester, vinyl ester, acrylamide, preferably N-vinyl lactams such as 3-methyl-N-vinylpyrrolidone, N-vinylcaprolactam and in particular N-vinylpyrrolidone.
  • the monomer mixture consisting of basic vinyl heterocycle, the crosslinking agent and, if appropriate, N-vinyllactam or another comonomer is rendered inert by introducing nitrogen and then heated to 100 to 200, preferably 150 to 180 ° C.
  • a weak stream of nitrogen is introduced into the mixture.
  • the batch is brought to the boil by applying a vacuum.
  • the mixture then polymerizes within 1 to 20 hours. For example, in the polymerization of 2-methyl-1-vinylimidazole with 2% N, N'-divinylethyleneurea at 150 ° C.
  • the first polymer particles slowly form after 2.5 h increase until after 10 h the mixture consists of a brownish powder. After washing with water and drying, the new polymer is obtained in yields of over 90% in the form of a coarse powder.
  • a preferred method of preparation is precipitation polymerization in water.
  • the concentration of the monomers in the reaction mixture is expediently chosen so that the mixture remains readily stirrable over the entire reaction period. If the water is too little, the polymer grains become sticky, so that stirring becomes more difficult than complete . without water.
  • the appropriate monomer concentration based on the aqueous mixture, is about 5 to 30, preferably 10 to 20,% by weight. They can be increased to 50% by weight if powerful agitators are available. It may also be appropriate to start the polymerization with a relatively concentrated solution and then to dilute it with water in the course of the reaction.
  • the polymerization is expediently carried out at pH values above 6 in order to avoid a possible saponification of the comonomers and / or crosslinking agents.
  • the pH can be adjusted by adding small amounts of bases such as sodium hydroxide or ammonia or the usual buffer salts such as soda, sodium hydrogen carbonate or sodium phosphate-J
  • the removal of oxygen can be achieved by keeping the polymerization batch at the boil and / or, as mentioned, using an inert gas such as nitrogen.
  • the polymerization temperature here can be 20 to 150 ° C. 50 to 100 ° C.
  • a reducing agent such as sodium sulfite, sodium pyrosulfite, sodium dithionite, ascorbic acid and the like in order to completely remove dissolved oxygen.
  • the water-soluble comonomer preferably an N-vinyl lactam
  • the crosslinking agent water and, if appropriate, a buffer and a reducing agent are heated in a gentle stream of nitrogen until the first polymer particles show up.
  • the polymer obtained with about 90 to 95% of the theoretical yield from the aqueous suspension can be isolated by filtration or centrifugation with subsequent washing out with water and drying in conventional dryers such as circulating air or vacuum drying cabinets, paddle dryers or current dryers.
  • the claimed polymers can generally be used as adsorber resins
  • phenolic substances such as tannin are adsorbed
  • colored accompanying substances can also be removed from sugar solutions by adsorption, and these polymers adsorb very well proteins, especially enzymes, which in many cases retain a considerable part of their activity even after adsorption with the adsorbed enzyme as a heterogeneous catalyst for the particular enzyme reaction, in which case the enzymes invertase, glucose isomerase, amyloglucosidase, alpha- and beta-amylase, amino acid acylase, penicillin acylase and hydantoinase are particularly preferred t: oxidoreductases - such as alcohol dehydrogenase, lactate dehydrogenase, amino acid oxidase, peroxidase, catechol oxidase, monoamine oxidase, lipoxygenase, luciferase, nitrate reduct
  • the polymers obtainable according to the invention are suitable for binding transition metal ions, e.g. Cu, Zn, Fe, Co, Ni, Ru, Rh, Pd, Pt, in different oxidation levels.
  • transition metal ions e.g. Cu, Zn, Fe, Co, Ni, Ru, Rh, Pd, Pt
  • These complexes can be used as catalysts in various reactions.
  • DE-OS 24 37 133 describes the carboxylation of alcohols in the presence of polyvinylpyridine-copper complexes.
  • pyridine-palladium complexes as catalysts in the production of isocyanates is e.g. known from DE-AS 24 16 683.
  • a polyvinylpyridine transition metal complex is specified as hydroformylation catalyst in US 3,652,676.
  • Example 2 As in Example 1, 75 parts of N-vinylimidazole, 25 parts of N-vinylpyrrolidone and 3 parts of N, N'-divinylethyleneurea were heated to boiling at 180 ° C. and 250 mbar with stirring. After about 1 hour the first polymer particles were visible, which grew quickly. After stirring for 2 hours, the mixture consisted of a dry powder. After washing and drying, 94 parts of a slightly yellow polymer were obtained.
  • the copolymer was in the form of a wet powder. After taking up in 2000 parts of water, the copolymer was centrifuged off, washed with 2000 parts of water and dried at 50 ° C. in a vacuum drying cabinet. The polymer was in the form of almost white, irregularly shaped aggregates of 0.1 to 3 mm in diameter. The yield was 90%.
  • Example 4 The polymerization was carried out as in Example 4, but 2-methyl-1-vinylimidazole was used as the monomer and N, N'-divinylpropyleneurea was used as the crosslinker. The yield was 96%.
  • an anion exchange capacity of 5.1 meq / g was achieved.
  • the polymerization was carried out as in Example 7, but after polymer particles had formed in the initial charge, a mixture of 1.05 parts of 1-vinyl-2-methylimidazole, 30 parts of vinyl acetate, 4.05 parts of N, N'-bisacryloyl ethylenediamine and 500 parts of water were added. The yield was 82.5%.
  • a polymer prepared according to Example 4 gave a water absorption of 1.7 g / g polymer using the same procedure.

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Abstract

A process for the preparation of insoluble, only slightly swellable, granular polymers of basic vinyl-heterocyclic compounds and of their copolymers with up to 30% by weight of copolymerizable monomers and 0.1-10% by weight of crosslinking agent by exclusion of (atmospheric) oxygen from the mixture of monomer and crosslinking agent, without addition of any initiator or catalyst, and the use of the polymers obtained as ion exchangers, adsorbents and carriers for proteins.

Description

Bekanntlich sind Homopolymere von N-Vinylimidazolen und Vinylpyridinen sowie deren Copolymere mit N-Vinyllactamen in Wasser und zahlreichen organischen Lösungsmitteln leicht löslich. Es ist auch bekannt, daß man unlösliche, aber quellbare Polymerisate von Vinylimidazolen bzw. Vinylpyridinen herstellen kann, indem man die Vinylheterocyclen in üblicher Art und Weise in Gegenwart mehrfunktioneller Monomerer (mit zwei oder mehr copolymerisierbaren Doppelbindungen), die vernetzend wirken, und gegebenenfalls einfach ungesättigter Comonomerer unter Zusatz von Radikalbildnern als Starter (oder Initiator genannt) polymerisiert. Als Vernetzer kommen beispielsweise in Frage Divinylester von Dicarbonsäuren wie Bernsteinsäure und Adipinsäure, Diacrylate von mehrwertigen Alkoholen wie Ethylenglykol und Butandiol, Allylether von mehrwertigen Alkoholen wie Pentaerythrittriallylether. Derartige Vernetzer sind nicht ganz einfach herzustellen und daher im Vergleich zu einfach ungesättigten Monomeren relativ teuer. Selbst bei Einsatz größerer Mengen des mehrfunktionellen Monomeren ist die Quellbarkeit der Polymeren in Wasser relativ hoch, so daß bei der Polymerisation in wäßriger Lösung ein Gel entsteht.As is known, homopolymers of N-vinylimidazoles and vinylpyridines and their copolymers with N-vinyllactams are readily soluble in water and numerous organic solvents. It is also known that insoluble but swellable polymers of vinylimidazoles or vinylpyridines can be prepared by customizing the vinyl heterocycles in the presence of polyfunctional monomers (with two or more copolymerizable double bonds) which have a crosslinking action and, if appropriate, monounsaturated Comonomer polymerized with the addition of radical formers as starters (or initiators). Possible crosslinkers are, for example, divinyl esters of dicarboxylic acids such as succinic acid and adipic acid, diacrylates of polyhydric alcohols such as ethylene glycol and butanediol, allyl ethers of polyhydric alcohols such as pentaerythritol triallyl ether. Crosslinkers of this type are not very easy to prepare and are therefore relatively expensive compared to monounsaturated monomers. Even when larger amounts of the multifunctional monomer are used, the swellability of the polymers in water is relatively high, so that a gel is formed during the polymerization in aqueous solution.

So lehrt die US-PS 2 878 183 die Herstellung von sehr stark vernetzten und daher unlöslichen, aber trotzdem stark quellbaren Polyvinylimidazolen durch radikalische Polymerisation von N-Vinylimidazolen in Gegenwart großer Mengen mehrfunktioneller Monomerer, wobei die Polymerisation in Wasser durchgeführt wird und die Polymeren als Gele anfallen. Solche stark quellbaren Gele haben sowohl bei ihrer Herstellung 'wie bei der allgemeinen Handhabung und bei der Anwendung als Ionenaustauscher oder als Träger für Reagentien wie Enzyme und dgl. schwerwiegende Nachteile: Sie verstopfen bei der Herstellung das Gefäß, können weder gerührt noch ausgeschüttet werden, und beim Trocknen müssen große Lösungsmittelmengen verdampft werden. Zum Gebrauch müssen sie vorgequollen werden und sind in diesem Zustand nicht schüttfähig; eine damit gefüllte Kolonne neigt zum Verstopfen.For example, US Pat. No. 2,878,183 teaches the production of very strongly crosslinked and therefore insoluble but nevertheless highly swellable polyvinylimidazoles by radical polymerization of N-vinylimidazoles in the presence of large amounts of polyfunctional monomers, the polymerization being carried out in water and the polymers as gels attack. Such highly swellable gels have both in their manufacture 'As with general handling and when used as an ion exchanger or as a carrier for reagents such as enzymes and the like. Serious disadvantages: they clog the vessel during manufacture, cannot be stirred or poured out, and large amounts of solvent have to be evaporated during drying. For use, they must be pre-swollen and are not pourable in this state; a column filled with it tends to clog.

Die DE-AS 19 29 501 beschreibt die Herstellung von Copolymeren aus N-Vinyllactamen mit geringen Mengen an N-Vinylimidazolen durch radikalische Polymerisation in Gegenwart von Vernetzern, wobei die Polymerisation in 10 bis 20 %igen wäßrigen Salzlösungen durchgeführt wird. Die Polymeren fallen dann in Form von Granulaten mit 1 bis 7 mm Durchmesser an. Nachteile dieses Verfahrens bestehen u.a. darin, daß die Isolierung der Polymeren in reiner Form aus der Salzlösung sehr aufwendig ist, und daß das Polymere in grober, nicht poröser Form und mit relativ geringer Oberfläche anfällt.DE-AS 19 29 501 describes the preparation of copolymers from N-vinyl lactams with small amounts of N-vinylimidazoles by radical polymerization in the presence of crosslinking agents, the polymerization being carried out in 10 to 20% strength aqueous salt solutions. The polymers are then obtained in the form of granules with a diameter of 1 to 7 mm. Disadvantages of this method include in that the isolation of the polymers in pure form from the salt solution is very complex and that the polymer is obtained in coarse, non-porous form and with a relatively small surface area.

Eine Methode zur Herstellung von Poly-N-vinylimidazolen beschreibt die DE-OS 23 24 204, wobei die Polymerisation in einem organischen Lösungsmittel erfolgt und es sehr aufwendig ist, die Polymeren in lösungsmittelfreier Form zu isolieren.DE-OS 23 24 204 describes a method for producing poly-N-vinylimidazoles, the polymerization being carried out in an organic solvent and it being very complex to isolate the polymers in solvent-free form.

Die DE-OS 25 06 085 lehrt die Polymerisation von Vinylimidazolen ohne Verwendung von Lösungsmitteln durch Photoinitiierung. Da die Polymerisate hierbei als Folien erhalten werden, ist ihr Einsatz stark eingeschränkt. Von Schwächen bei der Herstellung abgesehen, sind diese Polymerisate aufgrund ihrer relativ starken Quellbarkeit auch nur in begrenztem Maße als Ionenaustauscher oder Träger für Proteine geeignet.DE-OS 25 06 085 teaches the polymerization of vinylimidazoles without the use of solvents by photoinitiation. Since the polymers are obtained as films, their use is severely restricted. Apart from weaknesses in production, these polymers are only suitable to a limited extent as ion exchangers or carriers for proteins due to their relatively strong swellability.

Ein Verfahren zur Erzeugung relativ schwach quellbarer , Polymerisate, auch ohne Zusatz größerer Vernetzermengen ist in der Literatur u.a. als Popcorn-Polymerisation (H.F. Kauffmann und J. W. Breitenbach, Angew. Makromol. Ch. 45 (1975), 167 bis 175: N-Vinylpyrrolidon und Popcorn--Polymere; J.W. Breitenbach, H.F. Kauffmann und G. Zwilling, Makromol. Ch. 177 (1976), 2787 bis 2792: Acrylsäure-Popcorn-Polymere) oder im Englischen auch als Proliferous Polymerization (W. Breitenbach, Encycl. of Polymer Sci. and Technol. Vol. 11, 587 bis 597) bekannt. Diese Polymerisationsart, in der Technik als Störquelle bekannt, führt in der Regel zu technisch unbrauchbaren, unregelmäßig grobteiligen Produkten. Sie ist für basische Vinylheterozyklen bisher nicht bekannt.A method for producing relatively weak swellable polymers, even without the addition of greater amounts of crosslinker is, inter alia, in the literature as popcorn polymerization (HF Kauffmann and JW Breitenbach, Angew Makromol Ch 45 (1975), 167-175... N-vinylpyrrolidone and Popcorn - polymers; JW Breitenbach, HF Kauffmann and G. Zwilling, Makromol. Ch. 177 (1976), 2787 to 2792: acrylic acid popcorn polymers) or in English also as proliferous polymerization (W. Breitenbach, Encycl. Of Polymer Sci. And Technol. Vol. 11, 587 to 597). This type of polymerization, known in the art as a source of interference, generally leads to technically unusable, irregularly coarse-particle products. It is not yet known for basic vinyl heterocycles.

Der Erfindung lag die Aufgabe zugrunde, in möglichst einfacher Weise und unter Einsatz von möglichst geringen Mengen an (teuren) Vernetzern mit zwei oder mehr copolymerisierbaren Doppelbindungen porös körnige, in Wasser schwach quellbare, nicht gelbildende basische Polymere herzustellen, die als Ionenaustauscher und als Adsorberharze (Träger), insbesondere für Proteine (vor allem Enzyme), geeignet sind.The invention was based on the task of producing porous granular, water-swellable, non-gel-forming basic polymers in the simplest possible manner and using the smallest possible amount of (expensive) crosslinkers with two or more copolymerizable double bonds, which as ion exchangers and as adsorber resins ( Carrier), in particular for proteins (especially enzymes).

Die Lösung dieser Aufgabe wurde in dem Verfahren nach den Herstellansprüchen gefunden.The solution to this problem was found in the process according to the manufacturing claims.

Die erfindungsgemäß erhältlichen Polymeren unterscheiden sich von den "normalen", d.h. mit Hilfe von üblichen Mengen an Radikalbildnern als Startern oder durch Photoinitiierung erhaltenen Polymeren nicht nur dadurch, daß sie bei gleicher Vernetzerkonzentration wesentlich weniger in Wasser quellen, so daß die durch Quellung aufgenommene Wassermenge weniger als die Hälfte, in der Regel ein Drittel bis ein Siebentel oder noch weniger beträgt, sondern auch im , "gesamten Polymerisationsablauf und vor allem in ihrer optischen (makro- und mikroskopischen) Erscheinung: eine "normale" Polymerisation ohne Lösungsmittel ergibt einen festen Block, und in wäßriger Lösung im Falle der Wasserlöslichkeit von Monomer und Polymer (wie im vorliegenden Fall) ein Gel, während hier in beiden Fällen eine poröse, körnige Masse mit einem Korndurchmesser im Bereich von etwa 10 bis 500pm entsteht. Wird ohne Rühren polymerisiert, so verbacken die Körner zu einem porösen Kuchen, der sich leicht zerkrümeln läßt. Wird während der Polymerisation gerührt, was stets vorzuziehen ist, so agglomerieren die Körner lose zu unregelmäßig geformten Krümeln, deren durchschnittliche Größe von der Rührintensität abhängt und meist in der Größenordnung von 0,1 bis 5 mm Durchmesser liegt.The polymers obtainable according to the invention differ from the "normal", that is to say with the aid of customary amounts of free radical formers as starters or polymers obtained by photoinitiation not only in that they swell considerably less in water at the same crosslinker concentration, so that the amount of water taken up by swelling is less than half, usually a third to a seventh or even less, but also in, " overall course of the polymerization and above all in its optical (macro- and microscopic) appearance: a" normal "polymerization without solvent results in a solid block, and in aqueous solution if the monomer and polymer are water-soluble (as in the present case) a gel, while in both cases a porous, granular mass with a grain diameter in the range of about 10 to 500 pm is formed. If polymerization is carried out without stirring, the grains bake into a porous cake which can be easily crumbled. If the mixture is stirred during the polymerization, whatever it is preferable that the grains agglomerate loosely into irregularly shaped crumbs, the average size of which depends on the intensity of stirring and is usually in the order of 0.1 to 5 mm in diameter.

Die Polymerisation des Monomeren/Vernetzer-Gemisches beginnt, sobald der Luftsauerstoff vollständig entfernt ist, spontan selbst bei Raumtemperatur und sogar ohne daß die Polymerisationsinhibitoren, beispielsweise Hydrochinon, t-Butylbrenzkatechin oder Phenothiazin, die die Monomeren normalerweise zur Erhöhung ihrer Lagerfähigkeit enthalten, entfernt worden wären. Molekularer Sauerstoff erscheint als der einzige Inhibitor, der nicht nur die normale radikalische, sondern auch die erfindungsgemäße Polymerisation inhibiert.The polymerization of the monomer / crosslinker mixture begins as soon as the atmospheric oxygen has been completely removed, spontaneously even at room temperature and even without the polymerization inhibitors, for example hydroquinone, t-butylpyrocatechol or phenothiazine, which the monomers normally contain to increase their shelf life, would have been removed . Molecular oxygen appears to be the only inhibitor that not only inhibits normal radical polymerization but also the polymerization according to the invention.

Aus dem deutschen Patent 24 37 629 ist ein Verfahren zur Herstellung von Klärungsmitteln für vegetabilische Getränke bekannt, demzufolge Mischungen von N-Vinyllactamen mit geringen Mengen eines zweifach ungesättigten cyclischen Säureamids als Vernetzer in Gegenwart bestimmter Schwefelverbindungen in verdünnter wäßriger Lösung nach der gleichen Polymerisationsmethode wie gemäß der vorliegenden Erfindung polymerisiert werden. Die so erhältlichen J Polymerisate adsorbieren besonders gut Gerbstoffe, jedoch nicht Proteine, sind also nicht als Träger für Enzyme, außerdem nicht als Ionenaustauscherharze geeignet.From German Patent 24 37 629 a process for the preparation of clarifiers for vegetable drinks is known, consequently mixtures of N-vinyl lactams with small amounts of a di-unsaturated cyclic acid amide as a crosslinking agent in the presence of certain sulfur compounds in dilute aqueous solution according to the same polymerization method as in the present invention can be polymerized. The J Polymers adsorb tannins particularly well, but not proteins, so they are not suitable as a carrier for enzymes, nor are they suitable as ion exchange resins.

Es ist das Verdienst der vorliegenden Erfindung, diese bei anderen Monomeren an sich bekannte, in der Regel aber nur unter negativen Aspekten betrachtete, weil als störend empfundene Polymerisationsart zum ersten Mal gezielt auf basische Vinylheterocyclen angewandt und dabei überraschend ein technisch fortschrittliches Ergebnis erreicht zu haben. Es gelingt erfindungsgemäß auf einfache Weise, die oben beschriebene Aufgabe zu lösen, d.h. in Wasser schwach quellbare und daher nicht gelbildende basische Polymere (und zwar gleich mit der erforderlichen großen Oberfläche) herzustellen, die als Ionenaustauscher und Adsorberharze hervorragend geeignet sind und ein breites Anwendungsspektrum haben.It is to the merit of the present invention that they have been known per se for other monomers, but as a rule only viewed from a negative point of view, because for the first time targeted polymerization of basic vinyl heterocycles as a type of polymerization which is perceived as disruptive and surprisingly achieved a technically advanced result. According to the invention, the task described above can be achieved in a simple manner, i.e. to produce basic polymers which are slightly swellable and therefore not gel-forming (and have the same large surface area), which are outstandingly suitable as ion exchangers and adsorber resins and have a wide range of applications.

Unter basischen Vinylheterocyclen sind hier gesättigte und aromatisch ungesättigte Heterocyclen mit einer Vinylgruppe und mindestens einem basischen tertiären Ring-Stickstoffatom mit einem pKa über 4, vorzugsweise im Bereich von 5 bis 8, zu verstehen. Außer der Vinylgruppe kann der Ring auch Alkylgruppen mit 1 bis 4 Kohlenstoffatomen, Phenyl-, Benzyl-Gruppen oder auch einen anellierten zweiten Ring tragen. Als Beispiele seien genannt:

  • N-Vinylimidazol sowie Derivate wie 2-Methyl-l-vinylimidazol, 4-Methyl-l-vinylimidazol, 5-Methyl-l-vinylimidazol, 2-Ethyl-l-vinylimidazol, 2-Propyl-1-vinylimidazol, 2-Isopropyl-1-vinylimidazol, 2-Phenyl-l-vinylimidazol, 1-Vinyl--4,5-benzimidazol, wobei N-Vinylimidazol und 2--Methyl-l--vinylimidazol besonders bevorzugt sind. Weiterhin können beispielsweise eingesetzt werden: 2-Vinylpyridin, 4-Vinylpyridin sowie 5-Methyl-2-vinylpyridin. Selbstverständlich können auch Gemische von basischen Vinylheterocyclen untereinander eingesetzt werden.
Basic vinyl heterocycles are to be understood here as meaning saturated and aromatically unsaturated heterocycles with a vinyl group and at least one basic tertiary ring nitrogen atom with a pKa above 4, preferably in the range from 5 to 8. In addition to the vinyl group, the ring can also carry alkyl groups with 1 to 4 carbon atoms, phenyl, benzyl groups or also a fused second ring. Examples include:
  • N-vinylimidazole and derivatives such as 2-methyl-1-vinylimidazole, 4-methyl-1-vinylimidazole, 5-methyl-1-vinylimidazole, 2-ethyl-1-vinylimidazole, 2-propyl-1-vinylimidazole, 2-isopropyl 1-vinylimidazole, 2-phenyl-1-vinylimidazole, 1-vinyl-4,5-benzimidazole, with N-vinylimidazole and 2-methyl-1-vinylimidazole being particularly preferred. The following can also be used, for example: 2-vinylpyridine, 4-vinylpyridine and 5-methyl-2-vinylpyridine. Of course Mixtures of basic vinyl heterocycles can also be used with one another.

Das Vernetzungsmittel wird in Mengen von 0,1 bis 10, vorzugsweise 1 bis 4 %, bezogen auf das Gesamt-Monomerengewicht, verwendet. Geeignete Vernetzer sind solche, die zwei oder mehr copolymerisierbare Gruppen im Molekül enthalten. Besonders geeignet sind Alkylenbisacrylamide wie Methylenbisacrylamid und N,N'-Bisacryloylethylendiamin, außerdem N,N'-Divinylethylenharnstoff, N,N'-Divinylpropylenharnstoff, Ethyliden-bis-3-(N-vinylpyrrolidon) sowie N,N'-Divinyldi- imidazolyl(2,2') und 1,11-Bis(3,3'-vinylbenzimidazolid-2--on)-1,4-butan. Andere brauchbare Vernetzungsmittel sind beispielsweise Alkylenglykoldi(meth)acrylate wie Ethylen- glykoldi(meth)acrylat und Tetramethylenglykoldi(meth)acrylat, aromatische Divinylverbindungen wie Divinylbenzol und Divinyltoluol sowie Allylacrylat, Divinyldioxan, Pentaerythrit-triallylether und deren Gemische. Bei Polymerisation in Gegenwart von Wasser sind sie natürlich nur geeignet, soweit sie in der wäßrigen Monomermischung löslich sind.The crosslinking agent is used in amounts of 0.1 to 10, preferably 1 to 4%, based on the total monomer weight. Suitable crosslinkers are those which contain two or more copolymerizable groups in the molecule. Alkylenebisacrylamides such as methylenebisacrylamide and N, N'-bisacryloylethylenediamine, in addition N, N'-divinylethylene urea, N, N'-divinylpropylene urea, ethylidene-bis-3- (N-vinylpyrrolidone) and N, N'-divinyldimididazolyl ( 2,2 ') and 1,1 1- bis (3,3'-vinylbenzimidazolid-2 - one) -1,4-butane. Other useful crosslinking agents are, for example, alkylene glycol di (meth) acrylates such as ethylene glycol di (meth) acrylate and tetramethylene glycol di (meth) acrylate, aromatic divinyl compounds such as divinylbenzene and divinyltoluene, and allyl acrylate, divinyldioxane, pentaerythritol triallyl ether and mixtures thereof. In the case of polymerization in the presence of water, they are of course only suitable if they are soluble in the aqueous monomer mixture.

Das gleiche gilt selbstverständlich für die Comonomeren, die in Mengen bis zu 30, vorzugsweise bis zu 20 Gew.%, bezogen auf die gesamte Monomermischung, einpolymerisiert werden können. Als solche kommen beispielsweise in Betracht Styrol, Acrylester, Vinylester, Acrylamid, vorzugsweise N-Vinyllactame wie 3-Methyl-N-vinylpyrrolidon, N-Vinylcaprolactam und insbesondere N-Vinylpyrrolidon.The same naturally applies to the comonomers, which can be polymerized in amounts of up to 30, preferably up to 20,% by weight, based on the total monomer mixture. Examples include styrene, acrylic ester, vinyl ester, acrylamide, preferably N-vinyl lactams such as 3-methyl-N-vinylpyrrolidone, N-vinylcaprolactam and in particular N-vinylpyrrolidone.

Zur Durchführung der Polymerisation ohne Lösungsmittel wird das Monomerengemisch, bestehend aus basischem Vinylheterocyclus, dem vernetzenden Agens und gegebenenfalls N-Vinyllactam oder einem anderen Comonomeren durch Einleiten von Stickstoff inertisiert und anschließend auf 100 bis 200, vorzugsweise 150 bis 180°C erhitzt. Vorteilhaft ist es, wenn in die Mischung weiter ein schwacher Stickstoffstrom eingeleitet wird. Besonders vorteilhaft ist es, wenn der Ansatz durch Anlegen von Vakuum zum Sieden gebracht wird. Je nach Art der eingesetzten Monomeren und der gewählten Temperatur polymerisiert dann die Mischung innerhalb 1 bis 20 Stunden. Beispielsweise bilden sich bei der Polymerisation von 2-Methyl-l-vinylimidazol mit 2 % N,N'-Divinylethylenharnstoff bei 150°C unter Rühren mit einem kräftigen Rührwerk und einem Druck von 310 mbar nach 2,5 h die ersten Polymerisatteilchen, die langsam zunehmen, bis nach 10 h der Ansatz aus einem bräunlichen Pulver besteht. Nach Auswaschen mit Wasser und Trocknen wird das neue Polymere in Ausbeuten von über 90 % in Form eines groben Pulvers erhalten.To carry out the polymerization without a solvent, the monomer mixture consisting of basic vinyl heterocycle, the crosslinking agent and, if appropriate, N-vinyllactam or another comonomer is rendered inert by introducing nitrogen and then heated to 100 to 200, preferably 150 to 180 ° C. Advantageous it is if a weak stream of nitrogen is introduced into the mixture. It is particularly advantageous if the batch is brought to the boil by applying a vacuum. Depending on the type of monomers used and the temperature selected, the mixture then polymerizes within 1 to 20 hours. For example, in the polymerization of 2-methyl-1-vinylimidazole with 2% N, N'-divinylethyleneurea at 150 ° C. with stirring with a powerful stirrer and a pressure of 310 mbar, the first polymer particles slowly form after 2.5 h increase until after 10 h the mixture consists of a brownish powder. After washing with water and drying, the new polymer is obtained in yields of over 90% in the form of a coarse powder.

Eine bevorzugte Herstellungsart ist die Fällungspolymerisation in Wasser. Die Konzentration der Monomeren im Reaktionsansatz wird zweckmäßigerweise so gewählt, daß der Ansatz über die gesamte Reaktionsdauer hinweg gut rührbar bleibt. Bei zu wenig Wasser werden die Polymerisatkörner nämlich klebrig, so daß ein Rühren schwieriger wird als ganz.ohne Wasser. Bei den üblichen Rührkesseln liegt die zweckmäßige Monomerenkonzentration, bezogen auf die wäßrige Mischung, bei ca. 5 bis 30, vorzugsweise 10 bis 20 Gew.%. Man kann sie bis auf 50 Gew.% steigern, wenn kräftige Rührwerke zur Verfügung stehen. Es kann auch zweckmäßig sein, die Polymerisation mit einer relativ konzentrierten Lösung zu beginnen und dann im Verlauf der Reaktion mit Wasser zu verdünnen. Die Polymerisation wird ggf. zweckmäßigerweise bei pH-Werten über 6 durchgeführt, um eine eventuell mögliche Verseifung der Comonomeren und/oder Vernetzer zu vermeiden. Die Einstellung des pH-Wertes kann durch Zugabe geringer Mengen Basen wie Natriumhydroxid oder Ammoniak oder der üblichen Puffersalze wie Soda, Natriumhydrogencarbonat oder Natriumphos-J "phat erfolgen. Der Ausschluß von Sauerstoff läßt sich ' dabei dadurch erreichen, daß der Polymerisationsansatz am Sieden gehalten wird, und/oder wie erwähnt mit Hilfe eines Inertgases wie Stickstoff. Die Polymerisationstemperatur kann hier 20 bis 1500C betragen. Vorzugsweise arbeitet man bei 50 bis 100°C.A preferred method of preparation is precipitation polymerization in water. The concentration of the monomers in the reaction mixture is expediently chosen so that the mixture remains readily stirrable over the entire reaction period. If the water is too little, the polymer grains become sticky, so that stirring becomes more difficult than complete . without water. In the conventional stirred kettles, the appropriate monomer concentration, based on the aqueous mixture, is about 5 to 30, preferably 10 to 20,% by weight. They can be increased to 50% by weight if powerful agitators are available. It may also be appropriate to start the polymerization with a relatively concentrated solution and then to dilute it with water in the course of the reaction. If appropriate, the polymerization is expediently carried out at pH values above 6 in order to avoid a possible saponification of the comonomers and / or crosslinking agents. The pH can be adjusted by adding small amounts of bases such as sodium hydroxide or ammonia or the usual buffer salts such as soda, sodium hydrogen carbonate or sodium phosphate-J The removal of oxygen can be achieved by keeping the polymerization batch at the boil and / or, as mentioned, using an inert gas such as nitrogen. The polymerization temperature here can be 20 to 150 ° C. 50 to 100 ° C.

Bisweilen kann es von Vorteil sein, zur völligen Entfernung von gelöstem Sauerstoff geringe Mengen - 0,1 bis 1 Gew.%, bezogen auf die Monomermischung, - eines Reduktionsmittels wie Natriumsulfit, Natriumpyrosulfit, Natriumdithionit, Ascorbinsäure und dergleichen zuzusetzen.Sometimes it may be advantageous to add small amounts - 0.1 to 1% by weight, based on the monomer mixture, of a reducing agent such as sodium sulfite, sodium pyrosulfite, sodium dithionite, ascorbic acid and the like in order to completely remove dissolved oxygen.

Bei einer besonders bevorzugten Ausführungsform der Fällungspolymerisation wird das wasserlösliche Comonomere (vorzugsweise ein N-Vinyllactam), ein Teil des Vernetzers, Wasser und gegebenenfalls ein Puffer und ein Reduktionsmittel in einem schwachen Stickstoffstrom erhitzt, bis sich die ersten Polymerisatteilchen zeigen. Dann wird eine vorher durch Einblasen von Stickstoff inertisierte Mischung aus dem Vinylheterozyklus und dem restlichen Vernetzer und gegebenenfalls Wasser als Verdünnungsmittel innerhalb 0,2 bis 2 Stunden zugegeben. Diese Arbeitsweise hat den Vorteil, daß sich die Polymerisationszeiten verkürzen.In a particularly preferred embodiment of the precipitation polymerization, the water-soluble comonomer (preferably an N-vinyl lactam), part of the crosslinking agent, water and, if appropriate, a buffer and a reducing agent are heated in a gentle stream of nitrogen until the first polymer particles show up. Then a mixture of the vinyl heterocycle and the remaining crosslinking agent and, if appropriate, water, previously inertized by blowing in nitrogen, is added as the diluent within 0.2 to 2 hours. This procedure has the advantage that the polymerization times are shortened.

Die Isolierung des mit etwa 90 bis 95 % der theoretischen Ausbeute anfallenden Polymeren aus der wäßrigen Suspension kann durch Filtrieren oder Zentrifugieren mit anschließendem Auswaschen mit Wasser und Trocknen in üblichen Trocknern wie Umluft- oder Vakuumtrockenschrank, Schaufeltrockner oder Stromtrockner erfolgen.The polymer obtained with about 90 to 95% of the theoretical yield from the aqueous suspension can be isolated by filtration or centrifugation with subsequent washing out with water and drying in conventional dryers such as circulating air or vacuum drying cabinets, paddle dryers or current dryers.

Aufgrund des Gehaltes an basischem Stickstoff sind die beanspruchten Polymerisate in nicht quaternierter Form als schwache, in quaternierter Form als starke Anionenaus- "tauscher einsetzbar. Die Überführung in die quaternier- ' te Form mit üblichen Quaternierungsreagenzien wie Methyljodid oder Benzylchlorid führt zu Austauschkapazitäten bis zu etwa 6 mVal/g (Chlorid-Form). Abgesehen von ihrer Verwendbarkeit als Ionenaustauscher können die beanspruchten Polymerisate allgemein als Adsorberharze eingesetzt werden. Beispielsweise werden phenolische Substanzen wie Tannin adsorbiert. Ebenso können farbige Begleitsubstanzen aus Zuckerlösungen adsorptiv entfernt werden. Des weiteren adsorbieren diese Polymeren sehr gut Proteine, speziell Enzyme, welche in vielen Fällen auch nach der Adsorption einen beträchtlichen Teil ihrer Aktivität behalten. Sie können daher mit dem adsorbierten Enzym als heterogener Katalysator für die jeweilige Enzymreaktion eingesetzt werden. Besonders bevorzugt sind in diesem Fall die Enzyme Invertase, Glucoseisomerase, Amyloglucosidase, alpha- und beta-Amylase, Aminosäureacylase, Penicillinacylase und Hydantoinase. Ferner sind geeignet: Oxidoreduktasen - wie Alkoholdehydrogenase, Lactatdehydrogenase, Aminosäureoxidase, Peroxidase, Catecholoxidase, Monoaminooxidase, Lipoxygenase, Luciferase, Nitratreduktase, Nitritreduktase, Chlorperoxidase, Acetaldehyddehydrogenase, Aldehydoxigenase, Diaphorase, Cholesterinoxidase, Glutarthioreduktase, Hydroxysteroiddehydrogenase, Xanthinoxidase, Dopaminhydroxylase, Cytochromoxidase, Monoaminooxidase, Diacetylreduktase, Superoxiddismutase, Limonatdehydrogenase; Transferasen wie Polynucleotidphosphorylase, Dextransucrase, Phosphorylase, Carbamatkinase, Aminotransferase, Transaldolase, Methyltransferase, Pyruvatkinase, Carbamoyltransferase, Phosphofructokinase, Dextransynthetase; Hydrolasen wie Lipase, Esterase, Lactase, Lysozym, Cellulase, Urease, Trypsin, Chymotrypsin, Glutaminase, Asparaginase, Papain, Ficin, Pepsin, Leucinaminopeptidase, Carboxypeptidase A + B, Naringinase, Bromelain, Subtilisin, Phospholipase, Isoamylase, Cephalosporinamidase, L i Adenosindeaminase, Penicillinase, Maltase, Dextranase, Desoxyribonuclease, Sulfatase, Pullulanase, Phosphatase, alpha-Galactosidase, Dextranase, beta-Glucanase-; Lyasen wie Tryptophanase, Tyrosindecarboxylase, Oxinitrilase, Phenylalanindecarboxylase, Pyruvatdecarboxylase, Fumarase, Enolase, Aspartase, Aminolaevulindehydratase, Carboanhydratase; Isomerasen wie Aminosäureracemase, Triosephosphatisomerase; Ligasen wie Glutathionsynthetase.Due to the content of basic nitrogen, the claimed polymers are weak in non-quaternized form and strong anion in quaternized form. "Exchanger can be used. The conversion into the quaternized form with conventional quaternizing reagents such as methyl iodide or benzyl chloride leads to exchange capacities of up to about 6 meq / g (chloride form). Apart from their usability as ion exchangers, the claimed polymers can generally be used as adsorber resins For example, phenolic substances such as tannin are adsorbed, colored accompanying substances can also be removed from sugar solutions by adsorption, and these polymers adsorb very well proteins, especially enzymes, which in many cases retain a considerable part of their activity even after adsorption with the adsorbed enzyme as a heterogeneous catalyst for the particular enzyme reaction, in which case the enzymes invertase, glucose isomerase, amyloglucosidase, alpha- and beta-amylase, amino acid acylase, penicillin acylase and hydantoinase are particularly preferred t: oxidoreductases - such as alcohol dehydrogenase, lactate dehydrogenase, amino acid oxidase, peroxidase, catechol oxidase, monoamine oxidase, lipoxygenase, luciferase, nitrate reductase, nitrite reductase, chloroperoxidase, acetaldehyde, Aldehydoxigenase, diaphorase, cholesterol oxidase, Glutarthioreduktase, hydroxysteroid dehydrogenase, xanthine oxidase, Dopaminhydroxylase, cytochrome oxidase, monoamine oxidase, Diacetyl, superoxide dismutase , Limonate dehydrogenase; Transferases such as polynucleotide phosphorylase, dextransucrase, phosphorylase, carbamate kinase, aminotransferase, transaldolase, methyl transferase, pyruvate kinase, carbamoyl transferase, phosphofructokinase, dextran synthetase; Hydrolases such as lipase, esterase, lactase, lysozyme, cellulase, urease, trypsin, chymotrypsin, glutaminase, asparaginase, papain, ficin, pepsin, leucine aminopeptidase, carboxypeptidase A + B, naringinase, bromelain, subtilisin, phospholipase, isoamylase, Cephalosporinamidase, L i Adenosine deaminase, penicillinase, maltase, dextranase, deoxyribonuclease, sulfatase, pullulanase, phosphatase, alpha-galactosidase, dextranase, beta-glucanase; Lyases such as tryptophanase, tyrosine decarboxylase, oxinitrilase, phenylalanine decarboxylase, pyruvate decarboxylase, fumarase, enolase, aspartase, aminolaevulin dehydratase, carbonic anhydratase; Isomerases such as amino acid racemase, triose phosphate isomerase; Ligases such as glutathione synthetase.

Aufgrund der Neigung des zyklisch gebundenen basischen Stickstoffs zur Komplexbildung mit übergangsmetallen sind die erfindungsgemäß erhältlichen Polymeren zur Bindung von Übergangsmetallionen, z.B. Cu, Zn, Fe, Co, Ni, Ru, Rh, Pd, Pt, in verschiedenen Oxidationsstufen befähigt. Diese Komplexe können als Katalysatoren bei verschiedenen Reaktionen Verwendung finden. Beispielsweise wird in DE-OS 24 37 133 die Carboxylierung von Alkoholen in Gegenwart von Polyvinylpyridin-Kupfer-Komplexen beschrieben. Die Verwendung von Pyridin-Palladium-Komplexen als Katalysatoren bei der Herstellung von Isocyanaten ist z.B. aus DE-AS 24 16 683 bekannt. Des weiteren wird in US 3 652 676 als Hydroformylierungskatalysator ein Polyvinylpyridin--übergangsmetallkomplex angegeben.Due to the tendency of the cyclically bound basic nitrogen to form complexes with transition metals, the polymers obtainable according to the invention are suitable for binding transition metal ions, e.g. Cu, Zn, Fe, Co, Ni, Ru, Rh, Pd, Pt, in different oxidation levels. These complexes can be used as catalysts in various reactions. For example, DE-OS 24 37 133 describes the carboxylation of alcohols in the presence of polyvinylpyridine-copper complexes. The use of pyridine-palladium complexes as catalysts in the production of isocyanates is e.g. known from DE-AS 24 16 683. Furthermore, a polyvinylpyridine transition metal complex is specified as hydroformylation catalyst in US 3,652,676.

Weitere Einsatzgebiete für unlösliche Polymerisate mit basischem Stickstoff sind aus der Literatur bekannt. So weiß man, daß Polymerisate, die Imidazolringe enthalten, die Hydrolyse von z.B. Carbonsäureestern stark beschleunigen (R.L. Letsinger et al., J. Amer. Chem. Soc. 84 (1962) 3122). Polymere mit Pyridinringen sind zur Beschleunigung von Acylierungsreaktionen gut geeignet, wobei sie gleichzeitig zur Säurebindung dienen. Außerdem können Addukte von Polyvinylpyridin mit Brom für Bromierungen, solche mit Chromsäure für Oxidationen eingesetzt werden (J.M. Frechet et al., J. Macromol. Sci. Chem. 11 J (1977), 507; J.M. Frechet et al., J. Org. Chem. 43 (1978), ' 2618).Further areas of application for insoluble polymers with basic nitrogen are known from the literature. It is known, for example, that polymers containing imidazole rings greatly accelerate the hydrolysis of, for example, carboxylic acid esters (RL Letsinger et al., J. Amer. Chem. Soc. 84 (1962) 3122). Polymers with pyridine rings are well suited for accelerating acylation reactions, while at the same time they serve to bind acids. Adducts of polyvinylpyridine with bromine can be used for bromination and those with chromic acid for oxidation (JM Frechet et al., J. Macromol. Sci. Chem. 11 J (1977), 507; JM Frechet et al., J. Org. Chem. 43 (1978), '2618).

Die in den Beispielen genannten Teile und Prozente beziehen sich auf das Gewicht.The parts and percentages given in the examples relate to the weight.

Beispiel 1example 1

In einem Rührgefäß mit Rückflußkühler wurden 100 Teile frisch destilliertes 2-Methyl-l-vinyl-imidazol und 2 Teile N,N'-Divinylethylenharnstoff bei einem Druck von 310 mbar auf 150°C zum Sieden erhitzt. Nach 2,5 Stunden waren in der ursprünglich klaren Flüssigkeit kleine Polymerisatteilchen erkennbar, die langsam zunahmen. Nach 10 Stunden Rühren bestand der Ansatz aus einem trockenen Pulver. Nach Aufnehmen mit 1000 Teilen Wasser, Absaugen auf einer Nutsche, Nachwaschen mit 500 Teilen Wasser und Trocknen in einem Umluftschrank bei 50°C wurden 92 Teile eines leicht bräunlichen Polymerisats erhalten.In a stirred vessel with a reflux condenser, 100 parts of freshly distilled 2-methyl-1-vinylimidazole and 2 parts of N, N'-divinylethyleneurea were heated to boiling at 150 ° C. at a pressure of 310 mbar. After 2.5 hours, small polymer particles were visible in the originally clear liquid, which slowly increased. After stirring for 10 hours, the mixture consisted of a dry powder. After taking up with 1000 parts of water, suction filtration on a suction filter, washing with 500 parts of water and drying in a circulating air cabinet at 50 ° C., 92 parts of a slightly brownish polymer were obtained.

Beispiel 2Example 2

Wie bei Beispiel 1 wurden 75 Teile N-Vinylimidazol, 25 Teile N-Vinylpyrrolidon und 3 Teile N,N'-Divinylethylenharnstoff bei 180°C und 250 mbar unter Rühren zum Sieden erhitzt. Nach ca. 1 Stunde waren die ersten Polymerisatteilchen erkennbar, die schnell wuchsen. Nach 2 Stunden Rühren bestand der Ansatz aus einem trockenen Pulver. Nach Waschen und Trocknen wurden 94 Teile eines leicht gelben Polymeren erhalten.As in Example 1, 75 parts of N-vinylimidazole, 25 parts of N-vinylpyrrolidone and 3 parts of N, N'-divinylethyleneurea were heated to boiling at 180 ° C. and 250 mbar with stirring. After about 1 hour the first polymer particles were visible, which grew quickly. After stirring for 2 hours, the mixture consisted of a dry powder. After washing and drying, 94 parts of a slightly yellow polymer were obtained.

Beispiel 3Example 3

In einem Rührgefäß mit Rückflußkühler wurden 150 Teile frisch destilliertes N-Vinylimidazol, 3 Teile N,N'-Divinylethylenharnstoff und 50 Teile Wasser zum Sieden 'auf ca. 100°C erhitzt. Nach ca. 3 Stunden entstanden die ersten Polymerisatteilchen, nach 3,5 Stunden bestand der Ansatz aus einem dicken Polymerisatbrei. Nun wurde mit 500 Teilen Wasser verdünnt, wonach die Polymerisatteilchen weiter zunahmen. Nach insgesamt etwa 7 Stunden war die Reaktion beendet. Nun wurde auf einem Filter abgesaugt, das Polymere mit Wasser gewaschen und bei 50°C im Vakuumschrank getrocknet. Das Polymere lag in Form von fast weißen, unregelmäßig geformten Agglomerat-Teilchen von 0,5 bis 2 mm Durchmesser vor. Die Ausbeute betrug 92150 parts of freshly distilled N-vinylimidazole, 3 parts of N, N'-divinylethyleneurea and 50 parts of water were boiled in a stirred vessel with a reflux condenser 'heated to approx. 100 ° C. The first polymer particles formed after about 3 hours, after 3.5 hours the mixture consisted of a thick polymer slurry. The mixture was then diluted with 500 parts of water, after which the polymer particles continued to increase. The reaction was complete after a total of about 7 hours. It was then suctioned off on a filter, the polymer was washed with water and dried at 50 ° C. in a vacuum cabinet. The polymer was in the form of almost white, irregularly shaped agglomerate particles of 0.5 to 2 mm in diameter. The yield was 92

Beispiel 4Example 4

In einer Rührapparatur wurden 60 Teile N-Vinylpyrrolidon, 1,2 Teile N,N'-Divinylethylenharnstoff, 540 Teile destilliertes Wasser und 6,65 ml 0,1 n Natronlauge zum Sieden erhitzt. Nach 1/4 Stunde fielen unlösliche Polymerisatteilchen aus der Lösung aus. Nun wurde innerhalb 1,5 Stunden eine Mischung von 540 Teilen frisch destilliertem N-Vinylimidazol und 10,8 Teilen N,NI-Divinylethylenharnstoff zudosiert, wobei die Polymerisatteilchen sehr schnell zunahmen. Um die Suspension rührbar zu halten, wurde nach 1 Stunde, 2 Stunden und 3 Stunden mit jeweils 200 Teilen destilliertem Wasser verdünnt. Nach insgesamt 5 Stunden bei 100°C war die Polymerisation beendet. Das Copolymere lag in Form eines feuchten Pulvers vor. Nach Aufnehmen in 2000 Teilen Wasser wurde das Copolymere abzentrifugiert, mit 2000 Teilen Wasser nachgewaschen und bei 50°C im Vakuumtrockenschrank getrocknet. Das Polymere lag in Form von fast weißen, unregelmäßig geformten Aggregaten von 0,1 bis 3 mm Durchmesser vor. Die Ausbeute betrug 90 %.60 parts of N-vinylpyrrolidone, 1.2 parts of N, N'-divinylethyleneurea, 540 parts of distilled water and 6.65 ml of 0.1N sodium hydroxide solution were heated to boiling in a stirring apparatus. After 1/4 hour, insoluble polymer particles precipitated out of the solution. Now a mixture of 540 parts of freshly distilled N-vinyl imidazole and 10.8 parts of N, N I- Divinylethylenharnstoff was metered in over 1.5 hours, the polymer particles increased rapidly. In order to keep the suspension stirrable, the mixture was diluted with 200 parts of distilled water after 1 hour, 2 hours and 3 hours. The polymerization was complete after a total of 5 hours at 100.degree. The copolymer was in the form of a wet powder. After taking up in 2000 parts of water, the copolymer was centrifuged off, washed with 2000 parts of water and dried at 50 ° C. in a vacuum drying cabinet. The polymer was in the form of almost white, irregularly shaped aggregates of 0.1 to 3 mm in diameter. The yield was 90%.

15 Teile des nach Beispiel 4 erhaltenen Polymerisats wurden mit 25 Teilen Methyliodid in 200 Teilen Ethanol 5 Stunden auf 600C erhitzt. Danach wurde abgesaugt, mit Ethanol gewaschen und bei 50°C im Vakuum getrocknet. Nach überführung in die Chloridform wies das quaternierte Polymere eine Anionenaustauschkapazität von 5,0 mVal/g auf.15 parts of the polymer obtained according to Example 4 were mixed with 25 parts of methyl iodide in 200 parts of ethanol Heated to 60 0 C for 5 hours. It was then filtered off, washed with ethanol and dried at 50 ° C in a vacuum. After conversion to the chloride form, the quaternized polymer had an anion exchange capacity of 5.0 meq / g.

Beispiel 5Example 5

In einer Rührapparatur wurden 60 Teile 4-Vinylpyridin, 1,2 Teile N,N'-Divinylethylenharnstoff, 540 Teile destilliertes Wasser und 6,8 Teile 0,1 n Natronlauge auf 80°C erwärmt. über das Gemisch wurde während der gesamten Reaktionszeit ein schwacher Stickstoffstrom geleitet. Nach 8 Stunden lag das Polymerisat in Form einer dicken Suspension vor. Das Polymere wurde auf einer Nutsche abgesaugt und mit 2000 Teilen Wasser gewaschen. Nach dem Trocknen bei 50°C im Vakuumtrockenschrank erhielt man ein fast weißes, körniges Produkt in einer Ausbeute von 90 %.60 parts of 4-vinylpyridine, 1.2 parts of N, N'-divinylethyleneurea, 540 parts of distilled water and 6.8 parts of 0.1N sodium hydroxide solution were heated to 80 ° C. in a stirring apparatus. A weak stream of nitrogen was passed over the mixture during the entire reaction time. After 8 hours the polymer was in the form of a thick suspension. The polymer was suction filtered on a suction filter and washed with 2000 parts of water. After drying at 50 ° C. in a vacuum drying cabinet, an almost white, granular product was obtained in a yield of 90%.

Beispiel 6Example 6

Die Polymerisation wurde wie in Beispiel 4 durchgeführt, jedoch wurde als Monomeres 2-Methyl-l-vinylimidazol und als Vernetzer N,N'-Divinylpropylenharnstoff verwendet. Die Ausbeute betrug 96 %. Durch Quaternierung eines Teils des Polymerisates analog Beispiel 4 wurde eine Anionen-Austauschkapazität von 5,1 mVal/g erzielt.The polymerization was carried out as in Example 4, but 2-methyl-1-vinylimidazole was used as the monomer and N, N'-divinylpropyleneurea was used as the crosslinker. The yield was 96%. By quaternizing part of the polymer analogously to Example 4, an anion exchange capacity of 5.1 meq / g was achieved.

100 mg des nicht quaternierten Polymerisates wurden in 100 ml einer 0,01 %igen Tanninlösung gerührt. Nach 10 Minuten wurde im überstand die Tanninkonzentration photometrisch bestimmt. Zu diesem Zeitpunkt waren bereits 20 % des Tannins am Polymeren adsorbiert. Nach 40 Minuten waren es 70 %.100 mg of the non-quaternized polymer were stirred in 100 ml of a 0.01% tannin solution. After 10 minutes, the tannin concentration in the supernatant was determined photometrically. At this point, 20% of the tannin was already adsorbed on the polymer. After 40 minutes it was 70%.

7 g des nicht quaternierten Polymerisates wurden 2 Tage in 70 ml einer 1 %igen Lösung von Invertase gerührt. Nach dieser Zeit waren 90 % des Enzyms gebunden. Danach wurde das Polymerisat in eine Säule überführt und bei 30°C mit einer Fließgeschwindigkeit von 100 ml/h eine 64 %ige Saccharose-Lösung darübergeleitet. Der Hydrolysegrad der Saccharose betrug nach 20 Tagen 81 %, nach 40 Tagen 80 %, nach 60 Tagen 80,5 %.7 g of the non-quaternized polymer were stirred for 2 days in 70 ml of a 1% solution of invertase. After this time, 90% of the enzyme was bound. The polymer was then transferred to a column and a 64% sucrose solution was passed over at 30 ° C. at a flow rate of 100 ml / h. The degree of hydrolysis of sucrose was 81% after 20 days, 80% after 40 days and 80.5% after 60 days.

Beispiel 7Example 7

In einer Rührapparatur wurden 15 Teile Vinylpyrrolidon, 0,45 Teile Divinylethylenharnstoff, 135 Teile Wasser und 1,65 Teile 0,1 n Natronlauge im Stickstoffstrom auf 85°C erhitzt. Nun wurden 0,03 Teile Natriumdithionit, gelöst in 10 Teilen Wasser, zugesetzt, und nach ca. 40 Minuten, als deutlich unlösliche Polymerisatteilchen erkennbar waren, wurde eine Mischung von 120 Teilen 1-Vinyl-2-methylimidazol, 15 Teilen Methylacrylat, 4,05 Teilen Methylenbisacrylamid und 500 Teilen Wasser innerhalb 20 Minuten zudosiert. Anschließend wurde noch 1 Stunde bei 85°C erhitzt. Nach Abkühlen wurde der dicke Polymerisatbrei abfiltriert, mit Wasser gewaschen und bei 50°C im Vakuumtrockenschrank getrocknet. Das Polymere lag in Form von weißen, unregelmäßig geformten Aggregaten von etwa 0,1 bis 5 mm Durchmesser vor. Die Ausbeute betrug 93,5 %.15 parts of vinylpyrrolidone, 0.45 part of divinylethyleneurea, 135 parts of water and 1.65 parts of 0.1N sodium hydroxide solution were heated to 85 ° C. in a nitrogen stream in a stirring apparatus. Now 0.03 parts of sodium dithionite, dissolved in 10 parts of water, were added, and after about 40 minutes, when clearly insoluble polymer particles were recognizable, a mixture of 120 parts of 1-vinyl-2-methylimidazole, 15 parts of methyl acrylate, 4, 05 parts of methylene bisacrylamide and 500 parts of water are metered in within 20 minutes. The mixture was then heated at 85 ° C for 1 hour. After cooling, the thick polymer slurry was filtered off, washed with water and dried at 50 ° C. in a vacuum drying cabinet. The polymer was in the form of white, irregularly shaped aggregates of approximately 0.1 to 5 mm in diameter. The yield was 93.5%.

Beispiel 8Example 8

Die Polymerisation wurde wie bei Beispiel 7 durchgeführt, jedoch nachdem in der Vorlage Polymerisatteilchen gebildet waren, wurde eine Mischung von 1,05 Teilen 1-Vinyl-2-methylimidazol, 30 Teilen Vinylacetat, 4,05 Teilen N,N'-Bisacrylo- ylethylendiamin und 500 Teilen Wasser zudosiert. Die Ausbeute betrug 82,5 %.The polymerization was carried out as in Example 7, but after polymer particles had formed in the initial charge, a mixture of 1.05 parts of 1-vinyl-2-methylimidazole, 30 parts of vinyl acetate, 4.05 parts of N, N'-bisacryloyl ethylenediamine and 500 parts of water were added. The yield was 82.5%.

Vergleichsbeispiel:Comparative example: Mit Radikalbildner hergestelltes vernetztes PolyvinylimidazolCrosslinked polyvinylimidazole produced with radical generator

100 Teile Vinylimidazol wurden mit 2 Teilen N,N'-Methylen- bisacrylamid und 2 Teilen Azodiisobuttersäurenitril in 500 Teilen Wasser gelöst und 4 h auf 80°C erwärmt. Das erhaltene steife Gel wurde im Vakuum bei 50°C getrocknet. Man erhielt ein glasartiges Polymerisat in nahezu quantitativer Ausbeute. Zur Bestimmung des Quellverhaltens wurde das Polymere zerkleinert, und eine Siebfraktion von 250 bis 500µm wurde in Wasser 2 h gequollen. Das gequollene Polymere wurde auf einer Nutsche scharf abgesaugt, feucht abgewogen, im Vakuum bei 80°C getrocknet und wieder gewogen. Es ergab sich eine Wasseraufnahme von 12,9 g/g Polymer.100 parts of vinylimidazole were dissolved in 500 parts of water with 2 parts of N, N'-methylene-bisacrylamide and 2 parts of azodiisobutyronitrile and heated to 80 ° C. for 4 hours. The stiff gel obtained was dried in vacuo at 50 ° C. A glass-like polymer was obtained in almost quantitative yield. To determine the swelling behavior, the polymer was comminuted and a sieve fraction of 250 to 500 μm was swollen in water for 2 hours. The swollen polymer was suctioned off sharply on a suction filter, weighed moist, dried in vacuo at 80 ° C. and weighed again. The water absorption was 12.9 g / g polymer.

Ein nach Beispiel 4 hergestelltes Polymerisat ergab bei gleichem Vorgehen eine Wasseraufnahme von 1,7 g/g Polymer.A polymer prepared according to Example 4 gave a water absorption of 1.7 g / g polymer using the same procedure.

Claims (18)

1. Verfahren zur Herstellung von unlöslichen, in Wasser nur wenig quellbaren,körnigen Polymerisaten eines basischen Vinylheterocyclus mit einem pKa > 4 und dessen Copolymerisaten mit bis zu 30 Gew.% copolymerisierbarer Monomerer durch Polymerisieren der Monomeren, gekennzeichnet durch die Kombination folgender Maßnahmen: - a) Einsatz von 0,1 bis 10 Gew.%, bezogen auf die Gesamtmonomermenge, eines Vernetzers, b) Ausschluß von Sauerstoff, c) Ausschluß von Polymerisationsinitiatoren. 1. Process for the production of insoluble, granular polymers of a basic vinyl heterocycle with a pKa> 4 and their copolymers with up to 30% by weight of copolymerizable monomers by polymerizing the monomers, characterized by the combination of the following measures: a) use of 0.1 to 10% by weight, based on the total amount of monomer, of a crosslinking agent, b) exclusion of oxygen, c) Exclusion of polymerization initiators. 2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß es in Gegenwart von Wasser bei 20 bis 150°C durchgeführt wird.2. The method according to claim 1, characterized in that it is carried out in the presence of water at 20 to 150 ° C. 3. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß es ohne Lösungsmittel bei 100 bis 200°C durchgeführt wird.3. The method according to claim 1, characterized in that it is carried out at 100 to 200 ° C without solvent. 4. Verfahren nach Anspruch 1 bis 3, dadurch gekennzeichnet, daß es in Gegenwart eines Reduktionsmittels durchgeführt wird.4. The method according to claim 1 to 3, characterized in that it is carried out in the presence of a reducing agent. 5. Verfahren nach Anspruch 1 bis 4, dadurch gekennzeichnet, daß als basischer Vinylheterocyclus 1-Vinylimidazol oder 2-Methyl-l-vinylimidazol eingesetzt wird.5. The method according to claim 1 to 4, characterized in that 1-vinylimidazole or 2-methyl-l-vinylimidazole is used as the basic vinyl heterocycle. 6. Verfahren nach Anspruch 1 bis 5, dadurch gekennzeichnet, daß als basischer Vinylheterocyclus 2-Vinylpyridin, 4-Vinylpyridin oder 2-Methyl-5-vinylpyridin eingesetzt wird.6. The method according to claim 1 to 5, characterized in that 2-vinylpyri as the basic vinyl heterocycle din, 4-vinylpyridine or 2-methyl-5-vinylpyridine is used. 7. Verfahren nach Anspruch 1 bis 6, dadurch gekennzeichnet, daß als Comonomeres ein N-Vinyllactam eingesetzt wird.7. The method according to claim 1 to 6, characterized in that an N-vinyl lactam is used as comonomer. 8. Verfahren nach Anspruch 1 bis 7, dadurch gekennzeichnet, daß als Comonomeres N-Vinylpyrrolidon eingesetzt wird.8. The method according to claim 1 to 7, characterized in that the comonomer used is N-vinylpyrrolidone. 9. Verfahren nach Anspruch 1 bis 8, dadurch gekennzeichnet, daß als Vernetzer N,N'-Divinylethylenharnstoff verwendet wird.9. The method according to claim 1 to 8, characterized in that N, N'-divinylethylene urea is used as crosslinker. 10. Verfahren nach Anspruch 1 bis 9, dadurch gekennzeichnet, daß die basischen Stickstoffatome der Vinylheterocyclen nach der Polymerisation mit einem üblichen Alkylierungsmittel vollständig oder teilweise quaterniert werden.10. The method according to claim 1 to 9, characterized in that the basic nitrogen atoms of the vinyl heterocycles are completely or partially quaternized after the polymerization with a conventional alkylating agent. 11. Verwendung der nach einem der Ansprüche 1 bis 10 hergestellten Polymeren als Ionenaustauscher.11. Use of the polymers produced according to one of claims 1 to 10 as an ion exchanger. 12. Verwendung der nach einem der Ansprüche 1 bis 10 hergestellten Polymeren als Adsorberharze.12. Use of the polymers produced according to one of claims 1 to 10 as adsorber resins. 13. Verwendung der nach einem der Ansprüche 1 bis 10 hergestellten Polymeren zur Adsorption von Proteinen aus wäßriger Lösung.13. Use of the polymers prepared according to one of claims 1 to 10 for the adsorption of proteins from aqueous solution. 14. Verwendung der nach einem der Ansprüche 1 bis 10 hergestellten Polymeren zur adsorptiven Immobilisierung von Enzymen.14. Use of the polymers prepared according to one of claims 1 to 10 for the adsorptive immobilization of enzymes. 15. Verwendung der nach einem der Ansprüche 1 bis 10 hergestellten Polymeren nach Adsorption eines Enzyms als heterogener Katalysator zur Durchführung der entsprechenden Enzymreaktion.15. Use of the polymers produced according to one of claims 1 to 10 after adsorption of an enzyme as a heterogeneous catalyst for carrying out the corresponding enzyme reaction. 16. Verwendung der nach einem der Ansprüche 1 bis 10 hergestellten Polymeren zur Bindung von übergangsmetallionen.16. Use of the polymers prepared according to one of claims 1 to 10 for binding transition metal ions. 17. Verwendung der nach einem der Ansprüche 1 bis 10 hergestellten Polymeren als Solvolysekatalysatoren.17. Use of the polymers produced according to one of claims 1 to 10 as solvolysis catalysts. 18. Verwendung der nach einem der Ansprüche 1 bis 10 hergestellten Polymeren als Acylierungskatalysatoren.18. Use of the polymers prepared according to one of claims 1 to 10 as acylation catalysts.
EP83102132A 1982-03-13 1983-03-04 Process for preparing insoluble, only slightly expandable polymers of basic vinyl-heterocyclic compounds, and their use Expired EP0088964B1 (en)

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EP0315831A2 (en) * 1987-11-04 1989-05-17 BASF Aktiengesellschaft Method for the production of a bioreactor and its use in the separation of racemic forms
EP0360276A2 (en) * 1988-09-22 1990-03-28 Kao Corporation Microbial adsorbent and microbial sensor using the same
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EP0455081A1 (en) * 1990-04-30 1991-11-06 BASF Aktiengesellschaft Hair fixing and hair care composition
EP0781787A2 (en) 1995-12-20 1997-07-02 Basf Aktiengesellschaft Heavy metal ions-polymer complexes and their use for selective removal of compounds from liquids
EP0846493A1 (en) * 1996-06-21 1998-06-10 Nippon Shokubai Co., Ltd. Liquid-absorbing resin, process for the preparation thereof, and gel composition
US6232373B1 (en) 1996-12-18 2001-05-15 Basf Aktiengesellschaft Production and use of formulations consisting of cellulose, kalium caseinate and cross-linked vinylpyrrolidone homopolymers and/or vinylimidazol/vinylpyrrolidone copolymers
US6525156B1 (en) 1999-05-07 2003-02-25 Basf Aktiengesellschaft Styrene-containing popcorn polymers, method for producing same and utilisation
WO2008148743A1 (en) 2007-06-06 2008-12-11 Basf Se Use of n-vinylimidazole polymers to improve the value-determining properties of biologic fermented solutions
DE202011005055U1 (en) 2011-04-12 2011-09-12 Basf Se Low-peroxide polymer containing phosphorus compound
EP2511331A1 (en) 2011-04-12 2012-10-17 Basf Se Low peroxide phosphorous compound contained polymers
US8623978B2 (en) 2010-11-23 2014-01-07 Basf Se Process for the preparation of low-peroxide crosslinked vinyllactam polymer
DE202015000809U1 (en) 2015-02-02 2015-02-16 Basf Se Copolymers containing Alkylaminoalkylalkoxy (meth) acrylates and their use for water treatment
US9023931B2 (en) 2011-04-12 2015-05-05 Basf Se Oxidation-sensitive, low-peroxide polymer comprising at least one inorganic phosphorus compound
DE112012001679B4 (en) 2011-04-12 2023-05-04 Basf Se Sealed packaging form filled with protective gas, containing an oxidation-sensitive, low-peroxide polymer, its use and method for stabilizing oxidation-sensitive polymers against peroxide formation

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Cited By (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0177812A1 (en) * 1984-09-18 1986-04-16 BASF Aktiengesellschaft Process for preparing insoluble, only slightly expandable polymers
EP0175335A1 (en) * 1984-09-18 1986-03-26 BASF Aktiengesellschaft Process for preparing insoluble, only slightly expandable polymers
EP0202606A2 (en) * 1985-05-17 1986-11-26 Tanabe Seiyaku Co., Ltd. Immobilized enzyme having reversible solubility
EP0202606A3 (en) * 1985-05-17 1989-03-15 Tanabe Seiyaku Co., Ltd. Immobilized enzyme having reversible solubility
EP0220593A1 (en) * 1985-10-19 1987-05-06 Hoechst Aktiengesellschaft Copolymer, process for its preparation and its use in the bonding of enzymes
EP0225829A2 (en) * 1985-11-29 1987-06-16 Universite De Paris Val-De-Marne (Paris Xii) Mineral carrier used in the chromatographic separation of proteins, and preparation process
FR2598512A1 (en) * 1985-11-29 1987-11-13 Paris Val Marne Universite USINABLE MINERAL SUPPORT FOR THE CHROMATOGRAPHIC SEPARATION OF PROTEINS, AND PROCESS FOR PREPARING THE SAME
EP0225829A3 (en) * 1985-11-29 1988-01-13 Universite De Paris Val-De-Marne (Paris Xii) Mineral carrier used in the chromatographic separation of proteins, and preparation process
FR2605237A1 (en) * 1986-10-20 1988-04-22 Centre Nat Rech Scient Support for the purification and separation of proteins, process of preparation and application in chromatography
EP0315831A3 (en) * 1987-11-04 1990-04-04 Basf Aktiengesellschaft Method for the production of a bioreactor and its use in the separation of racemic forms
EP0315831A2 (en) * 1987-11-04 1989-05-17 BASF Aktiengesellschaft Method for the production of a bioreactor and its use in the separation of racemic forms
EP0360276A3 (en) * 1988-09-22 1991-12-11 Kao Corporation Microbial adsorbent and microbial sensor using the same
EP0360276A2 (en) * 1988-09-22 1990-03-28 Kao Corporation Microbial adsorbent and microbial sensor using the same
DE4000978A1 (en) * 1990-01-16 1991-07-18 Basf Ag METHOD FOR REMOVING HEAVY METALIONS FROM WINE AND WINE-BASED BEVERAGES
EP0438713A2 (en) * 1990-01-16 1991-07-31 BASF Aktiengesellschaft Method for removing heavy metal ions from wine and related drinks
EP0438713A3 (en) * 1990-01-16 1991-10-30 Basf Aktiengesellschaft Method for removing heavy metal ions from wine and related drinks
US5094867A (en) * 1990-01-16 1992-03-10 Basf Aktiengesellschaft Removal of heavy metal ions from wine and wine-like beverages
EP0455081A1 (en) * 1990-04-30 1991-11-06 BASF Aktiengesellschaft Hair fixing and hair care composition
EP0781787A2 (en) 1995-12-20 1997-07-02 Basf Aktiengesellschaft Heavy metal ions-polymer complexes and their use for selective removal of compounds from liquids
EP0781787A3 (en) * 1995-12-20 1997-12-29 Basf Aktiengesellschaft Heavy metal ions-polymer complexes and their use for selective removal of compounds from liquids
US6103425A (en) * 1996-06-21 2000-08-15 Nippon Shokubai Co., Ltd. Liquid-absorbing resin, manufacturing method thereof and gel composition
EP0846493A4 (en) * 1996-06-21 1999-03-10 Nippon Catalytic Chem Ind Liquid-absorbing resin, process for the preparation thereof, and gel composition
EP0846493A1 (en) * 1996-06-21 1998-06-10 Nippon Shokubai Co., Ltd. Liquid-absorbing resin, process for the preparation thereof, and gel composition
US6232373B1 (en) 1996-12-18 2001-05-15 Basf Aktiengesellschaft Production and use of formulations consisting of cellulose, kalium caseinate and cross-linked vinylpyrrolidone homopolymers and/or vinylimidazol/vinylpyrrolidone copolymers
US6525156B1 (en) 1999-05-07 2003-02-25 Basf Aktiengesellschaft Styrene-containing popcorn polymers, method for producing same and utilisation
WO2008148743A1 (en) 2007-06-06 2008-12-11 Basf Se Use of n-vinylimidazole polymers to improve the value-determining properties of biologic fermented solutions
US8623978B2 (en) 2010-11-23 2014-01-07 Basf Se Process for the preparation of low-peroxide crosslinked vinyllactam polymer
DE202011005055U1 (en) 2011-04-12 2011-09-12 Basf Se Low-peroxide polymer containing phosphorus compound
EP2511331A1 (en) 2011-04-12 2012-10-17 Basf Se Low peroxide phosphorous compound contained polymers
US9023931B2 (en) 2011-04-12 2015-05-05 Basf Se Oxidation-sensitive, low-peroxide polymer comprising at least one inorganic phosphorus compound
DE112012001679B4 (en) 2011-04-12 2023-05-04 Basf Se Sealed packaging form filled with protective gas, containing an oxidation-sensitive, low-peroxide polymer, its use and method for stabilizing oxidation-sensitive polymers against peroxide formation
DE202015000809U1 (en) 2015-02-02 2015-02-16 Basf Se Copolymers containing Alkylaminoalkylalkoxy (meth) acrylates and their use for water treatment

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JPS58174406A (en) 1983-10-13
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JPH0339087B2 (en) 1991-06-12
ATE29220T1 (en) 1987-09-15
EP0088964A3 (en) 1984-12-05
EP0088964B1 (en) 1987-09-02
US4451582A (en) 1984-05-29

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